对叔丁基甲苯选择性氧化制对叔丁基苯甲醛催化剂研究--助剂T1的添加对催化剂结构及反应性能的影响

对叔丁基苯甲醛是香精香料及其它食用化工行业的重要原料 ,采用对叔丁基甲苯气相选择性氧化制对叔丁基苯甲醛可以克服对叔丁基苯甲醛生产过程中设备腐蚀严重、污染环境、工艺落后繁琐等缺点 ,所以一直是广大科技工作者十分关注的研究课题。迄今为止 ,国内外学者已有不少关于甲苯气相选择性氧化制苯甲醛的报道[1～ 3] ,但关于对叔丁基甲苯选择性氧化制对叔丁基苯甲醛的研究几乎未见报道。本文考察了在Ｖ -Ｃｓ -Ｃｕ体系催化剂上引入助剂Ｔ1后对催化剂反应性能的影响 ,结果发现助剂Ｔ1的添加对于提高对叔丁基苯甲醛的选择性具有明显的促进作…     

甲苯气相催化氧化合成苯甲醛的动力学

应用振动式内循环反应器进行了在V-H-3型催化剂上甲苯气相催化氧化合成苯甲醛的动力学研究。在350—400℃,甲苯分压为0.08—0.26大气压,氧分压为0.1—0.26大气压的范围内,该反应可用一个平行一连串反应历程来表示。各步反应均可用对于甲苯或苯甲醛为一级,对氧为半级反应来关联。建立了该反应系统的动力学模型,并将该模型计算值与100毫升催化剂单管试验结果进行了比较。     

气相色谱法测定甲苯氧化产物中的苯甲醛及苯甲酸

气相色谱法测定甲苯氧化产物中的苯甲醛及苯甲酸刘敬兰,周鸿娟（河北师范大学实验中心石家庄０５００１６）陈连文傅德才（河北经贸学院石家庄０５００６１）（河北轻化工学院石家庄０５００１８）１前言在由电化学间接氧化法从甲苯生产苯甲醛的反应过程中,反应条件及终点的控制直接影响着苯甲醛的回收率。苯甲醛及苯甲酸的测定方法虽已有报道〔１〕,但同时测定甲苯中两组分含量的方法尚未见报道。２实验部分（１）色谱条件：岛津气相色谱仪ＧＣ－１６Ａ,带Ｃ－Ｒ３Ａ数据处理机。     

薄层色谱分析在间-苯氧基苯甲醛合成中的应用

间-苯氧基苯甲醛是合成仿生农药拟除虫菊酯的重要原料。我们进行了间-苯氧基甲苯催化氧化合成间-苯氧基苯甲醛的研究。此反应速度快,氧化深度较难控制,因原料和产物沸点较高,用气相色谱指示反应进程较难达到要求。于是用薄层色谱指示反应进程,取得了令人满意的效果。另外还     

高效液相色谱法测定甲基苯甲醛异构体

甲苯羰基化产生P-甲基苯甲醛是重要的化工原料,Okami和吴达旭先后对甲苯同系物与三氯化铝的反应作了NMR研究,我们用新的催化体系研究了甲苯羰基化合成p-甲基苯甲醛,反应如下:     

V2O5-Ag2O/η-Al2O3催化剂上甲苯氧化制苯甲醛的研究

制备了一系列负载型V—Ag—Al—O催化剂并用于甲苯的气相选择氧化制苯甲醛反应，考察了催化剂组成对反应性能的影响．研究发现，V205负载量为12．5％、Ag2O负载量为7．5％并经773K活化的4号催化剂，在空速467．6h-1，温度663K时反应，得到了甲苯转化率49．58％、苯甲醛选择性29．22％的较好结果．用XRD、XPS、SEM等测试手段，对催化剂进行了结构表征．     

V2O5/高硅分子筛的酸性与甲苯气相选择氧化

用固体离子交换法制备了Ｖ２Ｏ５／ＺＳＭ－５和Ｖ２Ｏ５／丝光沸石两类催化剂。通过ＸＲＤ，ＬＲＳ，ＸＰＳ和Ｓｇ测定表征了Ｖ２Ｏ５在分子筛上的分散状态。用吡啶吸附红外光谱法和正丁胺非水溶液回滴法研究了催化剂的表面酸性。用ＥＳＲ研究了甲苯在催化剂上的吸附。结果表明，催化剂的酸性不同，它们吸附甲苯的能力也不同，对甲苯气相选择氧化的活性和选择性也有较大的差异。同时，甲苯选择氧化成苯甲醛的能力还与Ｖ２Ｏ５在分子     

甲苯异构体在石墨电极上的直接电氧化

通过循环伏安法、电化学原位红外光谱和恒电位电解法研究了甲苯异构体在0.05 mol/L硫酸体系中的直接电氧化行为. 结果表明, 对甲氧基甲苯、对甲基甲苯、对氯甲苯和对叔丁基甲苯4种含不同取代基的甲苯异构体具有相似的电氧化行为, 均在1710 cm^-1左右出现向下的羰基伸缩振动峰(υ_C=O), 在1130 cm^-1左右出现向上的甲基消耗峰. 通过气相色谱-质谱法(GC-MS)对恒电位电解产物进行检测, 进一步证实了在石墨电极、硫酸水溶液体系中甲苯异构体直接电氧化主要产物为相应的芳香醛, 40 ℃时, 对甲氧基苯甲醛的产率为70.9%.     

Ce_2Mo_3O_(12)超微粒子的制备及催化性能

以硝酸铈和钼酸铵为原料 ,采用溶胶 -凝胶法和微波加热技术制备了Ce2 Mo3 O12 超微粒子催化剂 ,使用DTA -TG ,IR ,XRD以及BET比表面测试等表征手段 ,考察了制备条件对复合氧化物超微粒子形成 ,晶相和比表面积的影响 .同时 ,测试了该样品对甲苯选择性氧化制苯甲醛反应的催化性能 .结果表明 :制备Ce2 Mo3 O12 超微粒子的适宜条件为 :初始溶液pH =1.0 ,柠檬酸 / (铈 +钼 )摩尔比等于 0 .4 ,在此条件下制得的干凝胶 ,经微波加热处理后 ,粒子的比表面积为 35 .8m2 /g ,粒径约为 4 0nm .在由甲苯气相选择氧化制苯甲醛的反应中表现出较好的催化活性     

取代芳烃电解氧化产物的GC-MS分析(Ⅱ)

采用GC-MS方法,分析了3种取代芳烃直接电解氧化的产物;从甲苯电解氧化产物中鉴定出7种主要成分,从对甲基苯甲醚电解氧化产物中鉴定出6种主要成分,从对叔丁基甲苯电解氧化产物中鉴定出6种主要成分;根据成分鉴定和含量测定结果,解释了以获取目标产物苯甲醛、对甲氧基苯甲醛和对叔丁基苯甲醛为目的的电解氧化反应要求。     

超细Fe-V-O催化剂上甲苯液相氧化制苯甲醛

分别采用共沉淀法,凝胶自燃烧法和水热法制备了Fe-V-O复合氧化物催化剂用于催化过氧化氢液相氧化甲苯制苯甲醛反应中,并采用N2等温吸附-脱附法,粉末X射线衍射,红外光谱,扫描电子显微镜,能量弥散X射线光谱和H2程序升温还原等方法对催化剂性质进行了表征.结果表明,制备方法显著影响催化剂的结构,比表面积,形貌,表面元素组成和还原性.Fe-V-O催化剂颗粒的超细化调变了其比表面积和还原性,从而改善了催化剂上甲苯液相氧化制苯甲醛反应性能.其中水热法制备的超细Fe-V-O催化剂具有最高的苯甲醛收率和较好的重复使用性能.这主要归因于该催化剂颗粒尺寸小,比表面积大,以及表面较多的活性钒氧物种和适宜的还原性.     

Dawson型杂多酸钕盐催化氧化甲苯制备苯甲醛

合成了Dawson型磷钼钒杂多酸稀土(钕)盐,并用红外光谱分析(IR)、X射线衍射(XRD)方法对催化剂进行了表征;以H2O2为氧化剂,进行了甲苯氧化制备苯甲醛的反应研究.由于钕和钒的协同作用,催化剂表现出高的活性.实验结果表明,甲苯的转化率90.1%,苯甲醛的选择性达51.0%,双氧水的转化率89.0%,双氧水的有效利用率43.1%.基于对杂多酸盐结构的研究,对反应机理进行了初步的探讨.     

A New Catalyst System V-Cs-Cu-Tl for Selective Oxidation of p-tert Butyl Toluene to p-tert Benzaldehyde

p-tert benzaldehyde is an important raw material of chemical industry. It is widely used in foodstuff, medicine and also used as intermediates of perfume. The conventional method of production of p-tert benzaldehyde resulted in waste water, which is easy to cause environmental pollution1-3. We tried to produce p-tert benzaldehyde from catalytic gas phase selective oxidation method. The study of the gas phase selective oxidation of p-tert butyl toluene to p-tert benzaldehyde is sparsely reporte…     

在线超声Mn~(3+)非均相氧化甲苯制备苯甲醛

在一定的硫酸浓度条件下,以高锰酸钾和硫酸锰为原料,采用均相液相氧化法获得了稳定性良好的Mn3+溶液。并以此溶液为氧化剂,在超声波作用下,选择性氧化甲苯制取苯甲醛。探讨了相关因素对Mn3+溶液的稳定性和苯甲醛收率的影响。实验结果表明,在硫酸浓度为4.0 mol/L,高锰酸钾和硫酸锰物质的量比为1∶12时,可制得浓度较高、稳定性良好的Mn3+溶液;同时在反应温度60℃,硫酸浓度7.0 mol/L,甲苯与Mn3+物质的量比4∶1时,施加59 kHz和175 W的超声波,可促进甲苯的选择性氧化,获得较高收率的苯甲醛。     

钴铝类水滑石液相选择性催化甲苯氧化合成苯甲醛

采用共沉淀法制备了不同Co/Al原子比的类水滑石（Cox/Al-LDHs,x=2、3和4）及其焙烧产物（Cox/Al-LDOs）,用XRD、FT-IR、BET及ICP等技术手段分别表征了催化剂的结构、组成和比表面积,考察了对甲苯选择性氧化制苯甲醛的催化性能。 结果表明,在优化条件甲苯0.6 mL（5.43 mmol）,催化剂Co4/Al-LDO 100 mg,过氧化氢叔丁醇21.7 mmol,溶剂乙腈10 mL,反应温度70 ℃,反应时间9 h下,甲苯的转化率为8.2%,苯甲醛的选择性达77.6%。 催化剂重复使用7次后其催化活性和选择性未见降低,使用前后催化剂的XRD谱图基本不变,显示较好的结构稳定性。     

Gas Phase Selective Catalytic Oxidation of Toluene to Benzaldehyde on V2O5-Ag2O／η-Al2O3 Catalyst

Gas phase selective catalytic oxidation of toluene to benzaldehyde was studied on V2O5-Ag2O/η-Al2O3 catalyst prepared by impregnation. The catalyst was characterized by XRD, XPS, TEM,and FT-IR. The catalytic results showed that toluene conversion and selectivity for benzaldehyde on catalyst sample No.4 (V/(V Ag)=0.68) was higher than other catalysts with different V/Ag ratios. This was attributed to the higher surface area, larger pore volume and pore diameter of the catalyst sample No.4 than the other catalysts. The XRD patterns recorded from the catalyst before and after the oxidation reaction revealed that the new phases were developed, and this suggested that silver had entered the vanadium lattice. XPS results showed that the vanadium on the surface of No.4 and No.5 sample was more than that in the bulk, thus forming a vanadium rich layer on the surface. It was noted that when the catalyst was doped by potassium promoter, the toluene conversion and selectivity for benzalde hydewere higher than those on the undoped catalyst. This was attributed to the disordered structure of V2O5 lattice of the K-doped catalyst and a better interfacial contact between the particles.     

Gas Phase Selective Catalytic Oxidation of Toluene to Benzaldehyde on V2O5-Ag2O/η-Al2O3 Catalyst

Gas phase selective catalytic oxidation of toluene to benzaldehyde was studied on V2O5-Ag2O/η-Al2O3 catalyst prepared by impregnation. The catalyst was characterized by XRD, XPS, TEM,and FT-IR. The catalytic results showed that toluene conversion and selectivity for benzaldehyde on catalyst sample No.4 (V/(V Ag)=0.68) was higher than other catalysts with different V/Ag ratios. This was attributed to the higher surface area, larger pore volume and pore diameter of the catalyst sample No.4 than the other catalysts. The XRD patterns recorded from the catalyst before and after the oxidation reaction revealed that the new phases were developed, and this suggested that silver had entered the vanadium lattice. XPS results showed that the vanadium on the surface of No.4 and No.5 sample was more than that in the bulk, thus forming a vanadium rich layer on the surface. It was noted that when the catalyst was doped by potassium promoter, the toluene conversion and selectivity for benzaldehyde were higher than those on the undoped catalyst. This was attributed to the disordered structure of V2O5 lattice of the K-doped catalyst and a better interfacial contact between the particles.     

Wavelength-dependent Photodissociation Dynamics of Benzaldehyde

The ultrafast dynamics of benzaldehyde upon 260, 271, 284, and 287 nm excitations have been studied by femtosecond pinup-probe time-of-flight mass spectrometry. A bi-exponential decay component model was applied to fit the transient profiles of benzaldehyde ions and fragment ions. At the S2 origin, the first decay of the component was attributed to the internal conversion to the high vibrational levels of S1 state. Lifetimes of the first component decreased with increasing vibrational energy, due to the influence of high density of the vibrational levels. The second decay was assigned to the vibrational relaxation of the S1 whose lifetime was about 600 fs. Upon 287 nm excitation, the first decay became ultra-short （-56 fs） which was taken for the intersystem cross from S1 to T2, while the second decay component was attributed to the vibrational relaxation. The pump-probe transient of fragment was also studied with the different probe intensity at 284 nm pump.